Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse* and G.L. Morrison** ** School of Mechanical and Manufacturing Engineering The University of New South Wales Sydney 2052 AUSTRALIA ∗ Engineering College The University of Asmara P.O. Box 1220 Asmara, ERITREA Abstract The performance of shallow solar pond batch water heaters has been investigated for hot water production in Sydney, Australia and Asmara, Eritrea. A simulation model was developed to predict the effect of different design parameters and different modes of operation on the long-term performance of the heaters. The simulation results indicate that shallow solar pond batch water heaters can be operated efficiently in multi-draw mode in summer and in single draw mode in winter. These heaters also perform well for process hot water supply with appropriate selection of pond water depth for a desired water temperature. 1 INTRODUCTION Among others, manufacturing and material costs, are the factors that hinder the application of solar hot water systems. Hence, design of low cost solar water heaters is crucial in harnessing solar energy economically. Shallow solar pond batch water heaters are low cost solar water heaters that can provide hot water in the range 35 °C to 75 °C. The proposed design of shallow solar pond batch water heaters is shown in fig 1. This design was proposed by Cohen (1978), Kudish et al (1978) , Garg et al (1982) and Sodha et al (1980). A typical design consists of a plastic bag with clear upper layer of 0.2 mm PVF (Tedlar) film and 0.55 mm bottom black film (such as chlorosulfonated polyethylene or polybutylene) placed in a horizontal tray. The bottom and sidewalls are insulated and the top is covered with either 3 mm ordinary glass or 0.2mm Tedlar film. In this design the insulation should be dense enough to withstand the weight of the water. The main purpose of the outer glazing in the two-cover design is to suppress heat losses. The choice of having either glass cover or Tedlar film as outer glazing material is governed by the desired service life and design cost of the heater. Glass as a cover material has good resistance to abrasion and extreme weather conditions in spite of low impact strength, high density and poor resistance to thermal stress Blaga (1978). Plastics such as Tedlar have superior transmission than glass for short wave radiation although it has higher long wave transmission and low strength (Lenel et al 1984). Outer Cover A simulation program was developed based on this typical design and the forgoing assumptions. The solar energy after being transmitted through the cover and water, which absorbs part of the solar radiation, is absorbed by the back surface. The major portion of the Insulation solar energy absorbed by the blackened back surface is transferred to the water while the rest is transferred through convection, radiation and conduction to the surrounding. The heat loss calculations include water Absorber convection heat loss from the outer cover and the Fig. 1. Schematic diagram of shallow solar conduction loss through the insulation are related to the pond batch water heater with glazing ambient temperature, wind speed and properties and thickness of insulation. Radiation heat exchange with the sky requires long wave radiation exchange models for clear and cloudy days, in this simulation program a clear sky radiation exchange model was used to account for the radiation Inner cover Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse and G.L. Morrison loss. The model can be used to determine the year round performance of the heaters under different operating conditions for different locations. The proposed design has also been investigated by Tsilingiris (1997) using a semi empirical model. This model uses an over-all top surface heat loss coefficient calculated from an empirical equation, including radiation exchange with the sky. 2 SIMULATION MODEL To simplify the calculations of the transient operation of shallow solar pond batch water heaters the following assumptions were made: • Reflection of solar radiation is uniform diffuse in character. • Solar radiation transmitted through the water body is absorbed completely by the back surface of the water. • Absorber surface, inner walls of the tank and water are at the same temperature. The thermal capacity of the plastic absorber and insulation are negligible compared to that of the water mass. The water surface is in close contact with the inner side of the cover and hence there is no air gap between the water and the inner cover. Thus, the water is suppressed from evaporation, which otherwise reduces the maximum temperature that can be achieved. The transmittance absorptance product of the system is calculated using the net radiation method. A FORTRAN computer program is developed to simulate the performance of the batch solar water heater described above. The useful energy collected (Qu) is calculated from an energy balance of short wave solar energy input S and the heat losses from the system. The overall heat loss coefficient is defined in terms of the cover temperature to avoid program instability due to negative values of radiation loss coefficient at sunrise especially in winter if defined in terms of ambient temperature. Qu = AS − AU w (t w − tc 2 ) − ( AU b + AsU s )(t w − ta ) (1) where Uw (W/m2 K) is the over all heat transfer coefficient from water to the outer cover, Ub (W/m2 K) is the heat loss coefficient through the bottom insulation and Us (W/m2 K) is the heat loss coefficient through the side wall insulation. U w = [1 / (hw + hrw ) + 1 / (hc1 + hr1 )] (2) U b = U s = ki / δ (3) −1 where hw (W/m2.K) is the convection heat transfer coefficient from the water to the inner cover, hrw (W/m2.K) is the radiation heat transfer coefficient from the absorber surface to the inner cover, kI (W/m.K) and δ( m) are thermal conductivity and the thickness of the insulation, A(m2) is the aperture area of the collector, As(m2) is the area of the side walls of the collector, tw, tc2 and ta are the water, outer cover and ambient air temperatures in K. The heat loss through the bottom and sidewalls of the heater was approximated by the conduction resistance of the insulation, the convection resistance to the surrounding was considered negligible. The net solar radiation received by the collector and useful energy collected are given by S = τα effb I b + τα effd I d (4) Qu = Mw Cpw dtw / dt (5) where ταeffb and ταeffd are the effective transmittance - absorptance product for beam and diffuse components, Ib and Id are the beam and diffuse components of solar radiation in W/m2, Mw is mass of water in the heater (kg) and Cpw (J/kg K) is the specific heat of water. 2 Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society Paper 100 Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse and G.L. Morrison The inner and outer cover temperatures ( tc1 and tc2 ) were calculated from equations (6) and (7) derived from energy balances for the covers, ( ) t c1 = (hw + hrw )t w + (α c1b I b + α c1d I d ) + (hr 1 + hc1 )t c 2 / (hr 1 + hc1 + hw + hrw ) ( ) t c 2 = U w t w + (α c 2b I b + α c 2d I d ) + hc 2 t a − q r 2 / (U w + hc 2 ) (6) (7) where αc1and αc2 are the absorptance of the inner and outer cover, respectively, hr1 (W/m2 K) is the radiation heat transfer coefficient between the two covers, hc1 (W/m2 K) is the convection heat transfer coefficient between the two covers, hc2 (W/m2 K) is the convection heat transfer coefficient from the cover to ambient air, qr2 (W) is the long wave radiation exchange between the outer cover and the sky. ( qr 2 = ε c 2σ t c 2 − t s 4 4 ) (8) εc2 is the emittance of the outer cover and ts (K)is temperature of the sky. The sky temperature is related to the dew point temperature as follows (Duffie 1991), t s = t a [0.711 + 0.005t dp + 0.000073t a 2 + 0.013 cos(15t m )]1/ 4 (9) where tdp (K) is the dew point temperature and tm (h) is the hour from midnight. The energy balance for the system gives the following solution for the rate of change of water temperature tw. dt w 1 A S − U w (t w − t c1 ) − U b + U s s (t w − t a ) = dt M w Cp w A (10) The analytical solution of eqn (9) gives the water temperature at the end of the time step and its average value for the time interval. The average water temperature is used to calculate film heat transfer coefficients. The effective transmittance - absorptance product of glazed solar pond batch water heaters was calculated using the net radiation method based on radiation intensity and physical properties of the covers and absorbing surface. The net radiation method produces a system of linear equations, which can be solved by matrix inversion to get the net radiation quantity reaching each surface. The individual heat transfer coefficients were calculated using the above eqns and correlation equations for the thermodynamic properties of water and air. The radiation heat transfer coefficient from the absorber surface to the inner cover hrw is given by hrw = σ 1 1 − 1 (t w 2 + t c1 2 )( t w + t c1 ) + ε a ε c1 (11) where σ is the Stefan Boltzmann constant, 5.67 x 10-8 W/m2.K4, εa is emissivity of the absorber and εc1 is emissivity of the inner cover. The convection heat loss coefficient from the water to the inner cover hw (W/m2 K) is calculated from film heat transfer equation for heat transfer from the top of a heated horizontal plate hw = Nuw k w Lw (12) 1 Nuw = 0.069 Ra 3 Pr 0.074 Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society (13) Paper 100 3 Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse and G.L. Morrison where kw (W/m K) is the thermal conductivity of water, Lw (m) is the pond water depth, Nuw is the Nusselt number for convection through water (Dropkin et al 1965), Ra is Rayleigh number, and Pr is Prandtl number for the water. The radiation heat transfer coefficient hr1 (W/m2 K) and convection heat transfer coefficient hc1 (W/m2 K) between the covers are given by hr 1 = σ 1 1 + − 1 (t c1 2 + t c 2 2 )(t c1 + t c 2 ) ε c1 ε c 2 hc1 = Nua k a (14) La (15) where ka (W/m2 K) is the thermal conductivity of air and La (m) is the air gap between the covers. The Nusselt number for heat transfer through the air gap between two parallel plates as given by Hollands et al (1976) is 1.6 1708 1708( sin 18 . θ) . 1 − Nua = 1 + 144 1 − Ra cosθ Ra cosθ + Ra cosθ 13 − 1 5830 + (16) where θ is the inclination of the plates to the horizontal. The “+ “ sign indicates that the expression is incorporated only if it is positive. The daily useful energy collected (Qud) is calculated from daily tap water temperature and daily maximum water temperature Qud = M w Cp w (t wm − t wo ) (17) The monthly useful energy Qum collected and monthly solar irradiation Hm is calculated by summing the daily values for the number of days in each month. The yearly useful energy collected Quy and yearly solar irradiation Hy and is determined by summing the monthly values. CALL DATA (Reads collector parameter and monthly water temperature ) CALL INITIAL ( Initializes starting conditions and monthly 3 energy parameter) COMPUTATION PROCEDURE The FORTRAN simulation program reads hourly meteorological data and computes the performance parameters for the water heater. The computation is performed using a small time step to reduce the error that can be introduced by assuming that the properties of water are constant over the computation time step. Then program then computes the incident angle and the transmittance absorptance product and the heat transfer coefficients and new water temperature by iteration. The average water temperature is used to calculate the heat transfer coefficients. Finally the useful energy, solar irradiation and useful energy collection efficiency of the system are evaluated. The computational procedure is given in fig 2. CALL READ (Reads hourly weather data) CALL INITIALD (Initializes hourly parameters) CALL ANGLE CALL TALF CALL HEATCO 4 RESULTS AND DISCUSSION To optimise the performance of shallow solar pond batch water heaters the proposed designs were investigated for glass and Tedlar as cover materials. In general plastics such as Tedlar, acrylic and Mylar have higher transmission than glass though they have short service life, low mechanical strength and high long wave transmission, which are undesirable properties. The transmittance absorptance product is CALL TEMP CALL ENERGYH (Calculates hourly energy parameter) NO Time=hour YES Time =End 4 Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society NO Paper STOP 100 Fig. 2. Shallow solar pond batch water Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse and G.L. Morrison higher for plastic covered heaters than for glass covered heaters. The annual useful energy collection efficiency of a heater operating in Sydney with a 5 cm pond water depth was found to be 46.5 % and 45.2 % for Tedlar and glass, respectively. For Asmara it was 44.8 % and 43.6 % for Tedlar and glass, respectively. Tedlar covered heaters show higher efficiency in both locations. However, the crucial factor in selecting the cover material is not only efficiency of the heater but also initial cost (which is higher for glass), ease of handling and installation and service life. The prime target of shallow solar pond batch water heaters being production of hot water at the lowest possible cost, plastics covers become the appropriate choice of cover material. 4.1 Single daily draw-off operation. The size of shallow solar pond batch water heaters investigated during simulation was 1.0x1.0 m2 aperture area, 40 mm cover spacing and various water depths. In order to determine the optimum pond water depth for a specific application the simulation model was run for a range of pond water depths for Asmara and Sydney weather conditions. The maximum daily pond water temperature for typical summer and winter days in Asmara is given in figs 3 and 4. The simulation results indicate that this heater can supply directly useable hot water at about 76 oC in December in Sydney and 70 oC in March in Asmara for 5 cm pond water depth. The pond water temperature produced in June in Sydney drops to about 33 oC, which is below the minimum hot water requirement for domestic applications. However, for Asmara in August and a 5 cm water depth the hot water temperature produced was about 55 oC, which is directly useable for domestic or other sector applications. Thus, shallow solar pond batch water heaters can be used to supply hot water through out the year in weather conditions such as Asmara. The model was also used to predict the grades of hot water produced by categorising the hot water in to temperature bands and summing up the useful energy collected in the temperature bands. In January and December in Sydney for 5 cm pond water depth 90 % of the hot water delivered was above 60 oC. For Asmara 85 % of the predicted hot water delivered throughout the year for 5 cm pond water depth was above 60 oC. 4.2 Multiple daily draw-off operation. Shallow solar pond batch water heaters can be operated in multi draw-off mode at water draw-off temperatures ranging from 40 oC to 55 oC. The predicted multi draw-off operation of a Tedlar covered heater for 45 oC water draw-off temperature and 4 cm water depth for Asmara is given in table 2. The results indicate that for 45 oC water temperature draw-offs can be made from two to three times a day in summer for 4 cm water depth in Sydney. But in winter multi draw operation is impossible in Sydney. In summer multi draw operation improves the collection efficiency. For Asmara for water temperature 45 oC and 4 cm pond water depth, draw-offs can be made twice a day through out a year. Water temperature, oC 80 w ater depth 15 cm 10 cm 5 cm 60 40 20 0 6 7 8 9 10 11 12 13 14 15 16 17 18 Time(hrs) Fig 3. Hourly pond water temperature in summer (March 23) for Asmara. Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society Paper 100 5 Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse and G.L. Morrison Water temperature, o C 60 water depth 15 cm 10 cm 5 cm 40 20 0 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 Time(hrs) Fig 4. Hourly pond water temperature in winter (August 31) for Asmara. Useful energy collected, MJ/m 2 500 400 300 w ater depth 15 cm 10 cm 5 cm 200 100 0 Jan Feb Mar Apr May Jun Jul Aug Sept Oct Nov Dec Fig 5. Monthly useful energy collected in Asmara (Tedlar cover). Daily average maximum water temperature, oC 80 60 40 w ater depth 15 cm 10 cm 5 cm 20 0 Jan Feb Mar Apr May Jun Jul Aug Sept Oct Nov Dec Fig 6. Monthly daily average maximum water temperature in Asmara (Tedlar cover). 6 Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society Paper 100 Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse and G.L. Morrison 80 Efficiency, % 60 40 water depth 15 cm 10 cm 5 cm 20 0 Jan Feb Mar Apr May Jun Jul Aug Sept Oct Nov Dec Fig 7. Monthly solar energy collection efficiency in Asmara (Tedlar cover). Table 2. Solar irradiation, useful energy collected and efficiency of shallow solar pond batch water heaters for multi-draw operation mode at 45 oC and 4 cm water depth for Asmara. Month Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec Solar irradiation MJ/m2 Qs 698.5 693.1 797.1 781.5 755.8 716.6 641.6 614.4 729.6 749.9 674.4 699.8 Useful energy MJ/m2 Efficiency, % Qu 329.0 308.1 388.9 368.2 346.7 314.8 268.7 248.9 332.8 342.1 293.4 323.8 η 47.1 44.5 48.8 47.1 45.9 43.9 41.9 40.5 45.6 45.6 43.5 46.3 Useful energy of last draw, MJ/m2 Qul 86.7 98.4 79.3 80.0 78.9 78.1 76.5 85.5 83.3 94.1 99.8 86.6 Number of draw-offs 60 58 76 74 72 68 58 50 67 69 57 61 η is monthly useful energy collection efficiency in multi-draw operation mode; and Qul is useful energy collected from the last draw each day and is not included in the efficiency calculation because the temperature of the last draw will be less than the required delivery temperature. 4.3 Effect of Insulation and Cover Spacing The effect of back and side insulation thickness was evaluated for heat loss coefficients (Ub = Us = 0.8 to 2.5 W/m2 K) corresponding to insulation thickness of approximately 50 to 15 mm. The performance of shallow solar pond batch water heaters was found to be not significantly effected less by the level of insulation. The solar energy collection efficiency for Sydney dropped by only 3.1 % and 4.4 % in winter and summer, respectively, when the bottom and side heat loss coefficient was increased from 0.8 to 2.5 (W/m2 K) for a water depth of 5 cm. Similarly, for 15 cm water depth the efficiency drops by only 0.23 % and 3.35 % for winter and summer. The drop in efficiency was 3.68 % and 3.92 % for winter and summer, respectively, for 5 cm pond water depth in Asmara. For 15 cm pond water depth the efficiency dropped by 2.22 % and 2.33 % for winter and Summer, respectively. These results indicate that insulation thickness of less than 15 mm is required. Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society Paper 100 7 Simulation of Shallow Solar Pond Batch Water Heaters B.A. Nigusse and G.L. Morrison The effect of cover spacing on the performance of shallow solar pond batch water heater has been investigated using the simulation model. The results for different cover spacing on a 5 cm deep pond indicate that cover spacing also has only a minor effect on the heater performance. The useful energy collection improved by about 1.3 % for cover spacing increase from 4 cm to 12 cm. Thus cover spacing should be no more than 40 mm. 5 CONCLUSIONS The long term performance of shallow solar pond batch water heaters has been investigated for Sydney and Asmara. This type solar heater has been shown to be suitable for hot water production for domestic and industrial applications at low initial capital cost. The following points can be drawn from the simulation results: 1. Hot water can be produced at temperatures above 70 oC for a pond water depth of 5 cm in summer (December) in locations such as Sydney however, the performance deteriorates in winter in Sydney. The daily average hot water temperature for 5 cm water depth in Sydney in June is only 33 oC. 2. Shallow solar pond batch water heaters perform well in locations like Asmara Eritrea throughout the year. The highest daily average water temperature produced is 76 oC for a 5 cm pond water depth in Summer (March and April) and the lowest daily average temperature is 57 oC in August. Thus, the hot water temperature produced by this type of solar water heater in Asmara in winter can be used directly for domestic applications or as industrial process feed water. 3. In multi-draw off operation mode shallow solar pond batch water heaters produce more useful energy than single draw operation due to reduced heat loss with the multi-draw operation. In summer in Sydney hot water can be drawn off up to three times a day at 45 oC for water depth of 5 cm. For a required delivery temperature of 50 oC water can be drawn from two to three times a day for a water depth of 5 cm in summer in Sydney. Shallow solar pond batch water heaters can not be operated in multi-draw mode in winter in Sydney. 4. Multi-draw operation of shallow solar pond batch water heaters is possible through out the year for locations such as Asmara. Hot water can be drawn two times a day at 45 oC for a 4 cm pond water depth in Asmara. 5. Shallow solar pond batch water heaters with plastic covers perform better than glass covered systems. As plastics are cheaper than glass it is recommended that shallow solar pond batch water heaters be constructed with a plastic outer cover. 6. Side and back heat losses do not significantly effect the performance of shallow solar pond batch water heaters. The energy collection efficiency drops by only 3.1 % and 4.4 % in winter and summer, respectively when the bottom and side heat loss coefficient is increased from 0.8 to 2.5 W/m2 K. To determine the optimum insulation thickness an economic analysis is required. 7. The performance of shallow solar pond batch water heaters is not significantly effected by cover spacing in the range of 20 to 40 mm. 8. Shallow solar pond batch water heaters perform better in locations near the equator since they must be installed horizontally. 9. The predicted annual useful energy collection efficiency of shallow solar pond batch water heaters with a Tedlar cover is 46.5 % and 45.2 % for Sydney and Asmara, respectively. 8 Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society Paper 100 Simulation of Shallow Solar Pond Batch Water Heaters 6 B.A. Nigusse and G.L. Morrison REFERENCES Blaga, A. (1978). Use of plastic in solar energy applications. Solar Energy, Vol. 21, 313 - 338. Chauhan, R.S. and Kadambi, V. (1976). Performance of a collector-cum-storage type of solar water heater. Solar Energy, Vol.18, 327-335. Cohen, A.B. (1978). Thermal optimisation of compact solar water heaters. Solar Energy, Vol. 20, pp.193-196, 1978. 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(1980). Physics of shallow solar pond water heaters. Int. J. of Energy Research, Vol.4, 323-337. Tsilingiris, P.T. (1997). Design, analysis and performance of low-cost plastic film large solar water heating systems. Solar Energy, Vol. 60, No. 5, 245 - 256. Proceedings of Solar ’97 - Australian and New Zealand Solar Energy Society Paper 100 9